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CN110050189A - The method of the concentration of the volatile organic compounds in fluid for controlling fluid network - Google Patents

The method of the concentration of the volatile organic compounds in fluid for controlling fluid network Download PDF

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CN110050189A
CN110050189A CN201780075670.1A CN201780075670A CN110050189A CN 110050189 A CN110050189 A CN 110050189A CN 201780075670 A CN201780075670 A CN 201780075670A CN 110050189 A CN110050189 A CN 110050189A
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A·布鲁什
Z·多康
I·博丹
N·努瓦永
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    • G01MEASURING; TESTING
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Abstract

本发明涉及一种用于监控网络的流体(11)中的有机化合物的浓度的方法,该流体(11)包含挥发性有机化合物,该方法包括以下步骤:·通过分析器(15)在线测量流体(11)中的有机化合物中的每种有机化合物的浓度(16)的第一步骤,·将由分析器(15)测量的每种有机化合物的浓度(16)与针对每种有机化合物的预定义阈值(160)进行比较的第二步骤,·如果至少一种由分析器(15)测量的有机化合物的浓度(16)大于对应的预定义阈值(160)则降低所述至少一种有机化合物的浓度的第三步骤。本发明还涉及一种用于监控有机化合物的浓度的装置(10)。

The invention relates to a method for monitoring the concentration of organic compounds in a fluid (11) of a network, the fluid (11) containing volatile organic compounds, the method comprising the steps of: Measuring the fluid on-line by an analyzer (15) The first step of the concentration of each of the organic compounds in (11) (16), the concentration (16) of each organic compound measured by the analyzer (15) is compared with the pre-defined values for each organic compound A second step in which thresholds (160) are compared, if the concentration (16) of at least one organic compound measured by the analyzer (15) is greater than a corresponding predefined threshold (160) reducing the concentration of the at least one organic compound The third step of concentration. The invention also relates to a device (10) for monitoring the concentration of organic compounds.

Description

用于控制流体网络的流体中的挥发性有机化合物的浓度的 方法for controlling the concentration of volatile organic compounds in fluids of fluid networks method

本发明属于在线测量流体网络中的有机化合物的领域并且涉及一种用于监控流体网络的流体中的有机化合物的浓度的方法。本发明还涉及一种用于监控流体网络的流体中的有机化合物的浓度的装置。本发明还可以应用于监控任何类型的流体,无论其是冷却的网络水、天然水、环境水或处理过的水,还是气态流体,例如空气。本发明适用于挥发性或非挥发性有机化合物。The present invention is in the field of on-line measurement of organic compounds in fluid networks and relates to a method for monitoring the concentration of organic compounds in fluids of a fluid network. The invention also relates to a device for monitoring the concentration of organic compounds in a fluid of a fluid network. The invention can also be applied to monitor any type of fluid, whether it is cooled network water, natural, ambient or treated water, or gaseous fluids such as air. The present invention is applicable to volatile or non-volatile organic compounds.

饮用水由数十个非特异性参数(温度、pH、电导率、浊度等)、微生物参数(大肠杆菌、细菌总数等)以及有机化学参数(杀虫剂、烃、氯化溶剂、三卤甲烷等)和无机化学参数(金属、溴酸盐)等定义。合规性(compliance)借助于抽样和实验室分析来监控,其结果可以在从12小时至数周范围内的时间段内知晓。此外,对于大型设备,这些分析的频率可以在从每日(微生物,在大型设备处)到针对有机和无机化学参数的每月一次的最佳情况场景下改变。对于传送小于1000m3/日的设备来说,该频率可以仅是每年一次的。因此清楚的是,在这些实验室分析之间的间隔期间可能出现未被检测到的不一致的情形,因此可能无法在处理装置处采取动作。一种理想的解决方案可以包括利用通过在处理上游和/或下游的连续或半连续测量系统每日提供或者每天数次提供的信息来控制处理装置。Drinking water consists of dozens of non-specific parameters (temperature, pH, conductivity, turbidity, etc.), microbial parameters (E. coli, total bacteria, etc.), and organic chemical parameters (pesticides, hydrocarbons, chlorinated solvents, trihalomethanes, etc.) etc.) and inorganic chemical parameters (metals, bromates), etc. Compliance is monitored by means of sampling and laboratory analysis, the results of which can be known over time periods ranging from 12 hours to several weeks. Furthermore, for large facilities, the frequency of these analyses can vary from daily (microorganisms, at large facilities) to monthly best-case scenarios for organic and inorganic chemical parameters. For equipment transmitting less than 1000 m3 /day, this frequency may only be once a year. It is therefore clear that undetected inconsistencies may arise during the interval between these laboratory analyses and thus may not be able to take action at the processing device. An ideal solution may involve controlling the processing means with information provided daily or several times a day by continuous or semi-continuous measurement systems upstream and/or downstream of the processing.

对于有限数量的简单物理化学参数例如pH、浊度、导电率、温度、UV吸光度已经存在连续测量探头,但是至今还未发现能够监控有机化合物浓度的处理设备。Continuous measurement probes already exist for a limited number of simple physicochemical parameters such as pH, turbidity, conductivity, temperature, UV absorbance, but so far no processing equipment has been found capable of monitoring the concentration of organic compounds.

因此看起来有必要通过源自对具体(单独)有机化合物特别是挥发性有机化合物(VOC)的在线分析的信息来控制或优化处理装置。VOC在法国(第2006-623号法令)被定义为在101.3千帕的标准压力下测量具有小于或等于250℃的沸点的任何有机化合物(参见以下表格)。VOC由于其有毒性或者产生气味和臭味应当被考虑。与饮用水应用特别相关的化合物是那些在资源中最常出现的化合物,它们中的一些是被调控的(在以下表格中以黑体显示):氯乙烯、1,1-二氯乙烷、ETBE、1,1,1-三氯乙烷、氯仿、顺式-1,2-二氯乙烯、三氯乙烯以及四氯乙烯:It therefore appears necessary to control or optimize treatment plants by means of information derived from on-line analysis of specific (individual) organic compounds, especially volatile organic compounds (VOCs). A VOC is defined in France (Decree No. 2006-623) as any organic compound having a boiling point less than or equal to 250° C. (see table below), measured at a standard pressure of 101.3 kPa. VOCs should be considered because they are toxic or produce odors and odors. Compounds of particular relevance for drinking water applications are those most frequently found in the resource, some of which are regulated (shown in bold in the following tables): vinyl chloride, 1,1-dichloroethane, ETBE , 1,1,1-trichloroethane, chloroform, cis-1,2-dichloroethylene, trichloroethylene and tetrachloroethylene:

但是存在和实验室色谱仪的复杂性以及和为了使用它们所需要的专业知识有关的偏见。But there are biases related to the complexity of laboratory chromatographs and the expertise required to use them.

本发明旨在通过提供一种用于监控流体网络的流体中的有机化合物的浓度的方法来克服以上所述问题中的全部问题或一些问题,其通过对有机化合物执行在线测量并且其测量的结果使其能够控制工业方法以便在浓度过高的情况下降低有机化合物的该浓度。该方法使其能够改进来源于监控水网络的有机化合物的数据的可操作使用。其能够确保和实验室参照方法的性能相同的性能(具有相对低的最大可允许偏差),并且因此能够在没有因旨在降低有机化合物浓度而对产品过度计量或欠计量的风险下优化处理线的可操作参数。The present invention aims to overcome all or some of the above-mentioned problems by providing a method for monitoring the concentration of organic compounds in the fluids of a fluid network by performing on-line measurements of organic compounds and the results of their measurements This makes it possible to control industrial processes in order to reduce this concentration of organic compounds if the concentration is too high. This method makes it possible to improve the actionable use of data derived from monitoring organic compounds of water networks. It ensures the same performance as the laboratory reference method (with a relatively low maximum allowable deviation) and thus enables the optimization of the process line without the risk of over- or under-dosing of the product aimed at reducing the concentration of organic compounds operational parameters.

为此目的,本发明的一个主题是一种用于监控工业设备的流体网络的流体中的有机化合物的浓度的方法,该流体包含多种有机化合物,其特征在于该方法包括以下步骤:To this end, a subject of the present invention is a method for monitoring the concentration of organic compounds in a fluid of a fluid network of an industrial plant, the fluid containing a plurality of organic compounds, characterized in that the method comprises the following steps:

·通过分析器在线测量流体网络的流体中的多种有机化合物中的每种有机化合物的浓度的第一步骤,a first step of measuring the concentration of each of the plurality of organic compounds in the fluid of the fluid network online by an analyzer,

·将由分析器测量的多种化合物中的每种有机化合物的浓度与针对每种有机化合物的预定义阈值例如处理设定点值或者最大报警值进行比较的第二步骤,a second step of comparing the concentration of each of the plurality of compounds measured by the analyzer to a predefined threshold for each organic compound, such as a treatment setpoint value or a maximum alarm value,

·如果至少一种由分析器测量的有机化合物的浓度大于对应的预定义阈值则降低所述至少一种有机化合物的浓度的第三步骤。• A third step of reducing the concentration of the at least one organic compound if the concentration of the at least one organic compound measured by the analyzer is greater than a corresponding predefined threshold value.

根据一个实施方式,降低第三步骤包括将具有降低至少一种有机化合物的浓度的效果的产品注入流体网络的步骤。其可以是将反应物(例如,吸附介质、氧化剂、汽提气)注入流体网络或者使用处理方法(例如,膜过滤)的步骤。According to one embodiment, the third step of reducing comprises the step of injecting a product having the effect of reducing the concentration of at least one organic compound into the fluid network. It can be the step of injecting reactants (eg, adsorption media, oxidant, stripping gas) into the fluid network or using a treatment method (eg, membrane filtration).

根据一个实施方式,工业设备旨在执行工业方法,并且降低第三步骤包括作用于至少一个该工业方法中具有降低所述至少一种有机化合物的浓度的效果的参数。According to one embodiment, the industrial plant is intended to perform an industrial process, and reducing the third step comprises acting on at least one parameter in the industrial process which has the effect of reducing the concentration of said at least one organic compound.

根据另一实施方式,在降低第三步骤之前根据本发明的监控方法包括将由分析器测量的多种有机化合物中的每种有机化合物的浓度远程传输至控制中心的步骤。According to another embodiment, the monitoring method according to the invention, before the third step of reducing, comprises the step of remotely transmitting the concentration of each of the plurality of organic compounds measured by the analyzer to a control center.

根据一个实施方式,该工业方法是一种利用按照液态流体和气态流体之间预定义比例的气态流体通过曝气来处理液态流体的方法,并且降低第三步骤包括根据在网络的流体中测量的至少一种挥发性有机化合物的浓度的变化而调整液态流体和气态流体之间的所述比例。According to one embodiment, the industrial method is a method of treating a liquid fluid by aeration using a gaseous fluid in a predefined ratio between the liquid fluid and the gaseous fluid, and the third step of reducing comprises according to a measurement in the fluid of the network. The change in the concentration of the at least one volatile organic compound adjusts the ratio between the liquid fluid and the gaseous fluid.

根据另一实施方式,该工业方法是利用钻井液的钻井方法,并且降低第三步骤包括根据在网络的流体中测量的所述至少一种有机化合物的浓度的变化而调整钻井液的密度和/或成分。According to another embodiment, the industrial method is a drilling method utilizing a drilling fluid, and the third step of reducing comprises adjusting the density and/or the density of the drilling fluid as a function of a change in the concentration of the at least one organic compound measured in the fluid of the network. or ingredients.

根据另一实施方式,该工业方法是用于通过添加至少一种氧化反应物给水消毒的方法,并且降低第三步骤包括根据在网络的流体中测量的至少一种有机化合物浓度的变化而调整所添加的至少一种反应物(例如氯)的量。According to another embodiment, the industrial method is a method for sanitizing water by adding at least one oxidizing reactant, and the third step of reducing includes adjusting the concentration of at least one organic compound measured in the fluid of the network The amount of at least one reactant (eg, chlorine) added.

根据另一实施方式,该工业方法是用于处理饮用水的方法,该工业设备包括具有例如活性炭的颗粒状吸附介质的至少一个过滤器,或者注入例如活性炭的粉末状介质,并且降低第三步骤包括改变通过吸附剂/流体接触器的流体的流速的步骤,例如具有颗粒状吸附介质的过滤器、或者粉末状吸附介质/流体分隔器。粉末状吸附介质的计量还可以根据期望的有机化合物减少和根据在线监控进行调整。According to another embodiment, the industrial method is a method for treating drinking water, the industrial plant comprising at least one filter with a granular adsorption medium, such as activated carbon, or injecting a powdered medium, such as activated carbon, and reducing the third step Include the step of varying the flow rate of the fluid through the sorbent/fluid contactor, such as a filter with particulate sorbent media, or a powdered sorbent media/fluid divider. The metering of the powdered adsorption medium can also be adjusted according to the desired reduction of organic compounds and according to on-line monitoring.

有利地,降低第三步骤进一步包括再生过滤器介质的步骤并且介质的再生以固定的或可变的频率进行。Advantageously, the third step of lowering further comprises the step of regenerating the filter medium and the regeneration of the medium is performed at a fixed or variable frequency.

该工业处理方法还可以是基于可渗透液态流体的亲水性薄膜或者基于可渗透气态流体的疏水性薄膜的纳米过滤或反渗透类型的方法。The industrial treatment process can also be a nanofiltration or reverse osmosis type of process based on hydrophilic membranes permeable to liquid fluids or hydrophobic membranes permeable to gaseous fluids.

本发明还涉及一种用于监控适合于执行工业方法的工业设备的流体网络的流体中的有机化合物的浓度的装置,该流体包含多种有机化合物,该装置包括:分析器,该分析器定位在流体网络中的第一位置处,适合于在线测量第一位置处流体中的多种有机化合物中的每种有机化合物的浓度;比较器,该比较器适合于将由分析器测量的多种有机化合物中的每种有机化合物的浓度与针对每种有机化合物的预定义阈值进行比较;校正单元,该校正单元适合于如果由分析器测量的多种有机化合物中的至少一种有机化合物的浓度大于对应的预定义阈值则降低流体中所述至少一种有机化合物的浓度。The invention also relates to a device for monitoring the concentration of organic compounds in a fluid of a fluid network of industrial equipment suitable for performing an industrial process, the fluid containing a plurality of organic compounds, the device comprising: an analyzer positioned at a first location in the fluid network, adapted to measure online the concentration of each of the plurality of organic compounds in the fluid at the first location; a comparator adapted to measure the plurality of organic compounds to be measured by the analyzer the concentration of each of the organic compounds in the compound is compared to a predefined threshold for each organic compound; a correction unit adapted if the concentration of at least one of the plurality of organic compounds measured by the analyzer is greater than A corresponding predefined threshold reduces the concentration of the at least one organic compound in the fluid.

有利地,校正单元包括用于将具有降低所述至少一种有机化合物浓度的效果的产品注入流体网络的装置。Advantageously, the correction unit comprises means for injecting into the fluid network a product having the effect of reducing the concentration of said at least one organic compound.

根据一个实施方式,由于该工业方法涉及至少一个参数,所以校正单元包括第一控制模块,该第一控制模块配置为根据所测量的所述至少一种有机化合物的浓度变化而作用于该工业方法中具有降低所述至少一种有机化合物浓度的效果的至少一个参数。According to one embodiment, since the industrial process involves at least one parameter, the correction unit comprises a first control module configured to act on the industrial process as a function of the measured change in the concentration of the at least one organic compound has at least one parameter in the effect of reducing the concentration of the at least one organic compound.

根据另一实施方式,监控装置包括远程传输装置,该远程传输装置适合于将由分析器测量的多种有机化合物中的每种有机化合物的浓度远程传输至控制中心。According to another embodiment, the monitoring device comprises a remote transmission device adapted to remotely transmit the concentration of each of the plurality of organic compounds measured by the analyzer to a control center.

通过阅读以实施例的方式给出的实施方式的详细描述,可以更好地理解本发明并且其他优点将变得清楚明白,描述通过附图进行例示说明,其中:A better understanding of the invention and other advantages will become apparent on reading the detailed description of the embodiments, given by way of example, which is illustrated by the accompanying drawings, in which:

-图1示意性地表示了根据本发明的用于监控网络的流体中的有机化合物的浓度的方法的步骤,- Figure 1 schematically represents the steps of the method according to the invention for monitoring the concentration of organic compounds in the fluid of a network,

-图2示意性地表示了根据本发明的用于监控网络的流体中的有机化合物的浓度的装置的实施方式,- Figure 2 schematically represents an embodiment of the device according to the invention for monitoring the concentration of organic compounds in the fluid of a network,

-图3示意性地表示了根据本发明的用于监控网络的流体中的有机化合物的浓度的装置的另一实施方式。- Figure 3 schematically represents another embodiment of the device according to the invention for monitoring the concentration of organic compounds in the fluid of a network.

为清楚起见,在各个图中相同的元件将具有相同的附图标记。For the sake of clarity, identical elements will have the same reference numerals in the various figures.

图1,也另外参考图2,示意性地表示了根据本发明的用于监控网络的流体11中的有机化合物的浓度的方法的步骤。该方法用于监控工业设备的流体网络的流体11中的有机化合物的浓度,该流体11包含多种有机化合物,该方法包括:通过分析器15在线测量流体网络的流体11中的多种有机化合物中的每种有机化合物的浓度16的第一步骤1001,将由分析器15测量的多种有机化合物中的每种有机化合物的浓度16与针对每种有机化合物的预定义阈值160(例如,处理设定点值或最大报警值)进行比较的第二步骤1002,以及如果由分析器15测量的至少一种有机化合物的浓度16大于对应的预定义阈值160则降低所述至少一种有机化合物的浓度16的第三步骤1003。Figure 1, with additional reference also to Figure 2, schematically represents the steps of a method according to the invention for monitoring the concentration of organic compounds in a fluid 11 of a network. The method is used to monitor the concentration of organic compounds in a fluid 11 of a fluid network of industrial equipment, the fluid 11 containing a plurality of organic compounds, the method comprising: measuring the plurality of organic compounds in the fluid 11 of the fluid network online by an analyzer 15 A first step 1001 of the concentration 16 of each organic compound in the multiplicity of organic compounds measured by the analyzer 15 compares the concentration 16 of each organic compound in a second step 1002 of comparing a fixed point value or a maximum alarm value) and reducing the concentration of at least one organic compound if the concentration 16 of the at least one organic compound measured by the analyzer 15 is greater than the corresponding predefined threshold 160 The third step 1003 of 16.

分析器15配置为用于在线测量流体11中存在的多种有机化合物中的每种有机化合物的浓度16。这得到了多个浓度16,每一个针对所测量的每种有机化合物。并且对于每种有机化合物,预定义了阈值160,每一个值可能根据生效的标准而不同。将所测量的有机化合物的每个浓度与对应于所考虑的有机化合物的阈值进行比较。如果所测量的有机化合物的浓度大于该阈值,则需要对应于第三步骤1003的校正动作以用于降低该有机化合物的浓度。The analyzer 15 is configured for on-line measurement of the concentration 16 of each of the plurality of organic compounds present in the fluid 11 . This results in a number of concentrations 16, one for each organic compound measured. And for each organic compound, a threshold value 160 is predefined, each value may be different depending on the criteria in effect. Each concentration of the organic compound measured is compared to a threshold value corresponding to the organic compound under consideration. If the measured concentration of the organic compound is greater than the threshold, a corrective action corresponding to the third step 1003 is required for reducing the concentration of the organic compound.

降低第三步骤1003可以具体包括将具有降低所述至少一种有机化合物的浓度的效果的产品注入流体11的网络的步骤1004。产品的注入可以接受闭环控制,该闭环控制通过所测量的浓度与有机化合物的浓度的预定义阈值之间的差来进行控制。The third step 1003 of reducing may in particular comprise the step 1004 of injecting a product having the effect of reducing the concentration of said at least one organic compound into the network of fluid 11 . The injection of the product may be subject to closed-loop control by the difference between the measured concentration and a predefined threshold of the concentration of the organic compound.

根据本发明的监控方法可以包括在降低第三步骤1003之前将由分析器15测量的所述多种有机化合物中的每种有机化合物的浓度16远程传输至处理装置的控制中心的步骤1005。控制中心随后还可以作用于有机化合物的浓度,任选地通过人工干预。The monitoring method according to the present invention may comprise the step 1005 of remotely transmitting the concentration 16 of each of the plurality of organic compounds measured by the analyzer 15 to the control center of the processing device before the third step 1003 of reducing. The control center can then also act on the concentration of organic compounds, optionally by manual intervention.

本发明的一个特别有利的方面适用于旨在执行工业方法1000的工业设备9。根据本发明,降低第三步骤1003包括作用于工业方法1000中具有降低所述至少一种有机化合物的浓度16的效果的至少一个参数12,所述至少一种有机化合物的由分析器15测量的浓度大于其预定义阈值160。A particularly advantageous aspect of the invention applies to an industrial plant 9 intended to perform the industrial method 1000 . According to the invention, reducing the third step 1003 comprises acting on at least one parameter 12 in the industrial process 1000 having the effect of reducing the concentration 16 of the at least one organic compound whose value measured by the analyzer 15 The concentration is greater than its predefined threshold 160.

因此本发明通过对有机化合物浓度的在线测量使其能够在水和环境的世界中控制和优化工业方法(在性能和运行成本方面)。例如,本发明有助于防止由于水资源中的氯化溶剂所造成的工业污染从而改进处理系统。通过在上游控制工业设备的可操作参数,本发明使其能够监控氯消毒的副产物,例如三卤甲烷,其为挥发性有机化合物且为世界卫生组织的建议对象或者在美国、欧洲和澳大利亚具有限定值。在本发明的背景下,还能够识别和处理例如由废水工业以及生成嗅觉污染物的烂泥处理所产生的空气污染。The present invention thus makes it possible to control and optimize industrial processes (in terms of performance and operating costs) in the world of water and the environment through the on-line measurement of organic compound concentrations. For example, the present invention helps to improve treatment systems by preventing industrial pollution due to chlorinated solvents in water resources. By controlling the operational parameters of industrial equipment upstream, the present invention makes it possible to monitor by-products of chlorine disinfection, such as trihalomethanes, which are volatile organic compounds and are the subject of recommendations by the World Health Organization or have limit value. In the context of the present invention, it is also possible to identify and treat air pollution such as those produced by the wastewater industry and sludge treatment which generates olfactory pollutants.

根据一个实施方式,工业方法1000是一种用于通过利用按照液态流体和气态流体之间预定义比例的气态流体的曝气来处理液态流体的方法,并且降低第三步骤1003包括根据在网络的流体中测量的至少一种有机化合物的浓度的变化而调整液态流体和气态流体之间的比例。这导致了对处理方法(也被称为汽提方法)的效率的良好监控以及对其运行成本的优化。According to one embodiment, the industrial method 1000 is a method for treating a liquid fluid by aeration with a gaseous fluid in a predefined ratio between the liquid fluid and the gaseous fluid, and the third step 1003 of reducing comprises according to the Changes in the measured concentration of at least one organic compound in the fluid adjust the ratio between the liquid and gaseous fluids. This leads to good monitoring of the efficiency of the treatment process (also known as stripping process) and optimization of its operating costs.

根据另一实施方式,该工业方法是利用钻井液的钻井方法,并且降低第三步骤1003包括根据在网络的流体中测量的至少一种有机化合物的浓度的变化而调整钻井液的密度和/或成分。换言之,本发明通过利用已污染/未污染钻液的混合物实现了对已污染钻液的良好监控,以便符合和配水有关的法规。According to another embodiment, the industrial method is a drilling method utilizing a drilling fluid, and the third step 1003 of reducing comprises adjusting the density of the drilling fluid and/or the change in the concentration of at least one organic compound measured in the fluid of the network Element. In other words, the present invention achieves good monitoring of contaminated drilling fluids by utilizing a mixture of contaminated/uncontaminated drilling fluids in order to comply with regulations related to water distribution.

根据另一实施方式,该工业方法是用于通过添加至少一种反应物将水消毒的方法,并且降低第三步骤1003包括根据在网络的流体中测量的至少一种有机化合物的浓度的变化而调整所添加的至少一种反应物的量。According to another embodiment, the industrial method is a method for sterilizing water by adding at least one reactant, and the third step 1003 of reducing comprises varying the concentration of at least one organic compound measured in the fluid of the network The amount of at least one reactant added is adjusted.

根据另一实施方式,该工业方法是用于处理饮用水的方法,工业设备包括具有例如颗粒状活性炭的颗粒状吸附介质的至少一个过滤器,或者包括注入粉末状吸附介质,或者包括具有活性炭粉末状吸附介质的接触器或者薄膜分隔方法,并且降低第三步骤1003包括改变通过吸附剂/流体接触器的流体的流速的步骤,例如具有颗粒状吸附材料或介质的过滤器或者粉末状吸附介质/流体分隔器或者在具有粉末状吸附介质的接触器中。第三步骤1003还可以包括改变粉末状吸附介质的计量的步骤。也就是说,粉末状吸附介质的计量还可以根据期望的有机化合物减少和根据在线监控进行调整。According to another embodiment, the industrial method is a method for the treatment of drinking water, the industrial plant comprising at least one filter with a granular adsorption medium such as granular activated carbon, or with injection of a powdered adsorption medium, or with activated carbon powder Contactor or Membrane Separation Method of Adsorbent Media in Form of a Contactor, and the third step of reducing 1003 includes the step of changing the flow rate of the fluid through the sorbent/fluid contactor, such as a filter with particulate sorbent material or media or a powdered sorbent media/ Fluid separators or in contactors with powdered adsorption media. The third step 1003 may also include the step of changing the metering of the powdered adsorption medium. That is, the metering of the powdered adsorption medium can also be adjusted according to the desired reduction of organic compounds and according to on-line monitoring.

换言之,过滤器位于处理装置中。饮用水处理装置通常包括旨在消除微污染物的活性炭过滤器。通过作用于通过此类过滤器的水的流速以及它们的再生频率,能够改进对有机化合物的消除。还可以在设备中使用反应器以用于接触水/粉末状吸附介质,例如粉末状活性炭,其旨在消除微污染物。通过作用于通过此类接触器的水的流速以及对粉末状介质的计量,能够改进对有机化合物的消除。In other words, the filter is located in the processing device. Drinking water treatment units often include activated carbon filters designed to eliminate micro-pollutants. Elimination of organic compounds can be improved by acting on the flow rate of water passing through such filters and the frequency of their regeneration. Reactors can also be used in the plant for contacting water/powdered adsorption media, such as powdered activated carbon, which are designed to eliminate micro-pollutants. Elimination of organic compounds can be improved by acting on the flow rate of water through such contactors and the metering of the powdered medium.

有利地,降低第三步骤1003进一步包括再生过滤器介质的步骤1006并且介质的再生以固定的或可变的频率进行。Advantageously, lowering the third step 1003 further comprises a step 1006 of regenerating the filter media and the regeneration of the media is performed at a fixed or variable frequency.

工业方法(1000)还可以是用于处理饮用水的方法,工业设备包括至少一个可渗透液态流体的亲水性薄膜或者至少一个可渗透气态流体的疏水性薄膜,或者具有纳米过滤或反渗透类型。并且在这种情况下,降低第三步骤1003包括改变流体穿过薄膜的流速的步骤。The industrial method (1000) may also be a method for treating drinking water, the industrial device comprising at least one hydrophilic membrane permeable to liquid fluids or at least one hydrophobic membrane permeable to gaseous fluids, or of the nanofiltration or reverse osmosis type . And in this case, reducing the third step 1003 includes the step of changing the flow rate of the fluid through the membrane.

在由分析器15进行的测量之后,如果超过了调节值,则通过分析器15在线执行的测量的结果被用于对工业处理装置的操作通过例如降低氯的剂量、或者通过作用于凝聚剂的量或者粉末状活性炭的剂量或者作用于碳过滤器的再生频率优化对有机材料的消除而进行反馈。After the measurement by the analyzer 15, if the adjustment value is exceeded, the results of the measurement performed online by the analyzer 15 are used for the operation of the industrial treatment plant by, for example, reducing the dosage of chlorine, or by acting on the coagulant. The amount or dosage of powdered activated carbon or the frequency of regeneration acting on the carbon filter optimizes the elimination of organic materials in feedback.

根据本发明的方法的实施使其能够测量相关流体中有机化合物的浓度,因为其是在线地且连续地或半连续地执行,以及具有改进与流体相关联的工业方法的有用结果。The implementation of the method according to the invention makes it possible to measure the concentration of organic compounds in the relevant fluids, as it is performed in-line and continuously or semi-continuously, with useful results in improving industrial processes associated with fluids.

工业方法得到实时地控制,这使其面对任何可能的工业污染能够有更好反应性。这种实时控制在针对实验室中分析有机化合物浓度进行流体采样的情况下是不可想象的,因为周转时间过长。此外,由于有机化合物可能是挥发性有机化合物,对于实验室分析存在测量精度的问题,因为挥发性有机化合物极有可能不再存在于所分析的样本中。因此,根据本发明的对工业方法的控制通过实际地捕获污染物并且通过按照适当的方式对其处理使其能够与现实更为相关和接近。所得到的优点是节省了时间、成本以及流体处理的质量。The industrial process is controlled in real time, which makes it more responsive to any possible industrial pollution. Such real-time control is not conceivable in the case of fluid sampling for analyzing organic compound concentrations in the laboratory, due to the lengthy turnaround time. In addition, since organic compounds can be volatile organic compounds, there are measurement accuracy issues for laboratory analysis, as there is a high probability that volatile organic compounds are no longer present in the sample being analyzed. Therefore, the control of the industrial process according to the present invention makes it more relevant and closer to reality by actually capturing the pollutants and by treating them in an appropriate manner. The resulting advantages are savings in time, cost, and quality of fluid handling.

图2示意性地表示了根据本发明的用于监控网络的流体11中的有机化合物的浓度16的装置10的实施例。用于监控适合于执行工业方法1000的工业设备9的流体11的网络的流体11中的有机化合物的浓度16的装置10包括分析器15,该分析器定位在流体网络中的第一位置13处,适合于在线测量第一位置13处流体11中的多种有机化合物中的每种有机化合物的浓度16。分析器15是一种能够连续地或者半连续地在线测量在水或任何其他相关流体中被调节或者通常存在于其中的若干有机化合物。监控装置10包括:比较器17,该比较器适合于将由分析器15测量的多种有机化合物中的每种有机化合物的浓度16与针对每种有机化合物的预定义阈值160进行比较;以及校正单元18,该校正单元适合于如果由分析器15测量的多种有机化合物中的至少一种有机化合物的浓度大于对应的预定义阈值160则降低流体11中的至少一种有机化合物的浓度16。Figure 2 schematically represents an embodiment of a device 10 according to the invention for monitoring the concentration 16 of organic compounds in a fluid 11 of a network. Apparatus 10 for monitoring a concentration 16 of an organic compound in a fluid 11 of a network of fluids 11 of industrial equipment 9 suitable for performing industrial method 1000 includes an analyzer 15 positioned at a first location 13 in the fluid network , suitable for online measurement of the concentration 16 of each of the plurality of organic compounds in the fluid 11 at the first location 13 . The analyzer 15 is a type capable of continuous or semi-continuous on-line measurement of several organic compounds conditioned or normally present in water or any other relevant fluid. The monitoring device 10 comprises: a comparator 17 adapted to compare the concentration 16 of each of the plurality of organic compounds measured by the analyzer 15 with a predefined threshold 160 for each organic compound; and a correction unit 18. The correction unit is adapted to reduce the concentration 16 of at least one organic compound in the fluid 11 if the concentration of at least one organic compound of the plurality of organic compounds measured by the analyzer 15 is greater than a corresponding predefined threshold 160.

分析器15可以例如是连接至微量氩离子化检测器的包括采样装置的便携式气相色谱仪。分析器15可以包括两个探头,一个是温度探头而另一个允许氩气进入流体。两种类型的容器可以紧固到其上。一种被用于进行静态测试并且可以具有2L的容量。第二种容器被用于在线分析。其配备有两个开口,一个用作流体的入口而另一个用作出口,它们被连接至管以形成回路。有利地,分析器15在其被连接至电流出口时立即启动。数据处理在配备有与分析器15联网的合适软件的计算机上进行。其必须连接至氩气瓶以便进行操作。在线分析器能够在尽可能少的维护的情况下连续地操作。分析可以在没有对未重载的水预处理或预过滤的情况下进行。The analyzer 15 may, for example, be a portable gas chromatograph including a sampling device connected to a trace argon ionization detector. The analyzer 15 may include two probes, one being a temperature probe and the other allowing argon to enter the fluid. Two types of containers can be fastened to it. One is used for static testing and can have a 2L capacity. The second container is used for online analysis. It is equipped with two openings, one for the inlet of the fluid and the other for the outlet, which are connected to pipes to form a circuit. Advantageously, the analyzer 15 is activated as soon as it is connected to the current outlet. Data processing is carried out on a computer equipped with suitable software networked to the analyzer 15 . It must be connected to an argon cylinder for operation. On-line analyzers are able to operate continuously with as little maintenance as possible. Analysis can be performed without pre-treatment or pre-filtration of unreloaded water.

对于水的分析,水连续地循环通过下部单元。在可编程的频率下,循环水的有机化合物由惰性气体(在该情况下为氩气)汽提、由氩气通过捕获它们的吸附剂输送。后者随后被热解吸并且有机化合物由氩载气输送到将它们物理分离的色谱柱。被分离的化合物然后通过要求氩气用于其操作的微氩气离子检测器进行检测。这种系统因此根据动态顶部空间原理运行。For water analysis, water is continuously circulated through the lower unit. At a programmable frequency, the organic compounds of the circulating water are stripped with an inert gas (argon in this case), transported by the argon gas through an adsorbent that traps them. The latter is then thermally desorbed and the organic compounds are transported by an argon carrier gas to a chromatographic column where they are physically separated. The isolated compounds are then detected by a micro-argon ion detector that requires argon for its operation. Such a system thus operates according to the dynamic headspace principle.

应当注意,这是可以在本发明的背景下使用的分析器15的示例。本发明可以使用能够连续地或半连续地独立地在线分离有机化合物以便确定其浓度的任何类型的分析器实施。It should be noted that this is an example of an analyzer 15 that can be used in the context of the present invention. The present invention may be implemented using any type of analyzer capable of independently separating organic compounds on-line, continuously or semi-continuously, in order to determine their concentration.

有利地,校正单元18可以包括用于将具有降低所述至少一种有机化合物的浓度的效果的产品注入流体11的网络的装置。Advantageously, the correction unit 18 may comprise means for injecting into the network of fluid 11 a product having the effect of reducing the concentration of said at least one organic compound.

根据另一实施方式,监控装置10包括远程传输装置,该远程传输装置适合于将由分析器测量的多种有机化合物中的每种有机化合物的浓度16远程传输至控制中心。According to another embodiment, the monitoring device 10 includes a remote transmission device adapted to remotely transmit the concentration 16 of each of the plurality of organic compounds measured by the analyzer to a control center.

图3示意性地表示了根据本发明的用于监控网络的流体11中的有机化合物的浓度的装置10的另一实施方式。工业方法1000涉及至少一个参数12,校正单元18包括第一控制模块,该第一控制模块配置为作用于工业方法1000中具有根据所测量的所述至少一种有机化合物的浓度变化降低所述至少一种有机化合物的浓度的效果的至少一个参数12。Figure 3 schematically represents another embodiment of a device 10 according to the invention for monitoring the concentration of organic compounds in a fluid 11 of a network. The industrial method 1000 involves at least one parameter 12, and the calibration unit 18 includes a first control module configured to act in the industrial method 1000 to have a reduction in the at least one organic compound based on a change in the measured concentration of the at least one organic compound. At least one parameter 12 of the effect of the concentration of an organic compound.

因此,根据本发明的此类监控装置10使其能够获得对流体中有机化合物的浓度的在线测量、以及控制与流体相关联的工业方法。更具体地,此类监控装置使其能够通过作用于工业方法的工作参数以便在考虑由其所得到的有机化合物的水平的同时最佳地适应性调整工业设备的操作来识别并处理污染。如已经提到的,有机化合物可以是水中的氯化溶剂、三卤甲烷,而且也可以是特别专用于燃料的的添加剂,例如,乙基叔丁基醚(ETBE)或甲基叔丁基醚(MTBE),或者甚至是在分析器的检测阈值足够低的条件下有气味的藻代谢物。当然,本发明适用于任何的挥发性有机化合物。Thus, such a monitoring device 10 according to the present invention makes it possible to obtain on-line measurements of the concentration of organic compounds in fluids, as well as to control industrial processes associated with fluids. More specifically, such monitoring devices make it possible to identify and deal with contamination by acting on the operating parameters of the industrial process in order to optimally adapt the operation of the industrial plant while taking into account the levels of organic compounds derived therefrom. As already mentioned, the organic compounds can be chlorinated solvents in water, trihalomethanes, but also additives especially dedicated to fuels, for example, ethyl tert-butyl ether (ETBE) or methyl tert-butyl ether (MTBE), or even odorous algal metabolites under conditions where the analyzer's detection threshold is sufficiently low. Of course, the present invention is applicable to any volatile organic compound.

Claims (14)

1.一种用于监控工业设备(9)的流体网络的流体(11)中的挥发性有机化合物的浓度的方法,所述流体(11)包含多种挥发性有机化合物,其特征在于所述方法包括以下步骤:1. A method for monitoring the concentration of volatile organic compounds in a fluid (11) of a fluid network of an industrial plant (9), the fluid (11) comprising a plurality of volatile organic compounds, characterized in that the The method includes the following steps: ·第一步骤(1001):通过分析器(15)在线测量所述流体网络的所述流体(11)中的所述多种挥发性有机化合物中的每种挥发性有机化合物的浓度(16),a first step (1001): online measurement of the concentration (16) of each of the plurality of volatile organic compounds in the fluid (11) of the fluid network by an analyzer (15) , ·第二步骤(1002):将由所述分析器(15)测量的所述多种有机化合物中的每种挥发性有机化合物的所述浓度(16)与针对每种挥发性有机化合物的预定义阈值(160)例如处理设定点值或者最大报警值进行比较,a second step (1002): comparing the concentration (16) of each volatile organic compound in the plurality of organic compounds measured by the analyzer (15) with a predefined value for each volatile organic compound Thresholds (160) such as process setpoint values or maximum alarm values are compared, ·第三步骤(1003):如果由所述分析器(15)测量的至少一种挥发性有机化合物的所述浓度(16)大于对应的预定义阈值(160)则降低所述至少一种挥发性有机化合物的浓度。a third step (1003): reducing said at least one volatile organic compound if said concentration (16) of said at least one volatile organic compound measured by said analyzer (15) is greater than a corresponding predefined threshold (160) the concentration of sexual organic compounds. 2.根据权利要求1所述的监控方法,其特征在于所述降低第三步骤(1003)包括将具有降低所述至少一种挥发性有机化合物的浓度的效果的产品注入所述流体网络的步骤(1004)。2. The monitoring method according to claim 1, characterized in that the third step (1003) of reducing comprises the step of injecting into the fluid network a product having the effect of reducing the concentration of the at least one volatile organic compound (1004). 3.根据权利要求1和2中任一项所述的监控方法,所述工业设备(9)旨在实施工业方法(1000),其特征在于所述降低第三步骤(1003)在于作用于所述工业方法(1000)的具有降低所述至少一种挥发性有机化合物的浓度的效果的至少一个参数(12)。3. The monitoring method according to any one of claims 1 and 2, the industrial plant (9) intended to implement an industrial method (1000), characterized in that the third step (1003) of reducing consists in acting on the at least one parameter (12) of the industrial process (1000) having the effect of reducing the concentration of the at least one volatile organic compound. 4.根据前述权利要求中任一项所述的监控方法,其特征在于所述方法包括在所述降低第三步骤(1003)之前将由所述分析器(15)测量的所述多种挥发性有机化合物中的每种挥发性有机化合物的所述浓度(16)远程传输至控制中心的步骤(1005)。4. The monitoring method according to any one of the preceding claims, characterized in that the method comprises the plurality of volatiles to be measured by the analyzer (15) prior to the third step (1003) of reducing The step (1005) of remotely transmitting said concentration (16) of each volatile organic compound in the organic compound to a control center. 5.根据权利要求3和4中任一项所述的监控方法,其特征在于5. The monitoring method according to any one of claims 3 and 4, characterized in that ·所述工业方法(1000)是一种按照液态流体和气态流体之间预定义比例利用气态流体通过曝气来处理液态流体的方法,the industrial method (1000) is a method of treating a liquid fluid by aeration with a gaseous fluid according to a predefined ratio between the liquid fluid and the gaseous fluid, ·并且所述降低第三步骤(1003)在于根据在所述网络的流体中测量的所述至少一种挥发性有机化合物的浓度调节液态流体和气态流体之间的比例。and said third step (1003) of reducing consists in adjusting the ratio between liquid and gaseous fluids according to the concentration of said at least one volatile organic compound measured in the fluid of said network. 6.根据权利要求3和4中任一项所述的监控方法,其特征在于6. The monitoring method according to any one of claims 3 and 4, characterized in that ·所述工业方法(1000)是利用钻井液的钻井方法,the industrial method (1000) is a drilling method utilizing drilling fluid, ·并且所述降低第三步骤(1003)在于根据在所述网络的流体中测量的所述至少一种挥发性有机化合物的浓度调节所述钻井液的密度和/或组成。- and the third step (1003) of reducing consists in adjusting the density and/or composition of the drilling fluid according to the concentration of the at least one volatile organic compound measured in the fluid of the network. 7.根据权利要求3和4中任一项所述的监控方法,其特征在于7. The monitoring method according to any one of claims 3 and 4, characterized in that ·所述工业方法(9)是用于通过添加至少一种反应物将水消毒的方法,the industrial method (9) is a method for sterilizing water by adding at least one reactant, ·并且所述降低第三步骤(1003)在于根据在所述网络的流体中测量的所述至少一种挥发性有机化合物的浓度调整所添加的至少一种反应物的量。- and the third step (1003) of reducing consists in adjusting the amount of the at least one reactant added according to the concentration of the at least one volatile organic compound measured in the fluid of the network. 8.根据权利要求3和4中任一项所述的监控方法,其特征在于8. The monitoring method according to any one of claims 3 and 4, characterized in that ·所述工业方法(9)是用于处理饮用水的方法,所述工业设备包括具有颗粒状吸附介质的至少一个过滤器、或者具有活性炭粉末状吸附介质的接触器或薄膜分离方法,the industrial method (9) is a method for the treatment of drinking water, the industrial plant comprising at least one filter with a granular adsorption medium, or a contactor or a membrane separation method with an activated carbon powdered adsorption medium, ·并且所述降低第三步骤(1003)包括改变通过具有颗粒状吸附介质的所述过滤器的所述流体的流速或者在具有粉末状吸附介质的所述接触器中的所述流体的流速的步骤、或者包括改变所述粉末状吸附介质的计量的步骤。and said reducing the third step (1003) comprises varying the flow rate of said fluid through said filter with particulate adsorption medium or the flow rate of said fluid in said contactor with powdered adsorption medium step, or include the step of changing the metering of the powdered adsorption medium. 9.根据权利要求8所述的监控方法,其特征在于所述降低第三步骤(1003)进一步包括再生所述过滤器介质的步骤(1006)并且所述过滤器介质的再生以固定的或可变的频率进行。9. The monitoring method according to claim 8, characterized in that said lowering third step (1003) further comprises a step (1006) of regenerating said filter medium and the regeneration of said filter medium is fixed or variable variable frequency. 10.根据权利要求3和4中任一项所述的监控方法,其特征在于:10. The monitoring method according to any one of claims 3 and 4, wherein: ·所述工业方法(9)是用于处理饮用水的方法,所述工业设备包括至少一个可渗透液态流体的亲水性薄膜或者至少一个可渗透气态流体的疏水性薄膜,the industrial method (9) is a method for treating drinking water, the industrial equipment comprising at least one hydrophilic membrane permeable to liquid fluids or at least one hydrophobic membrane permeable to gaseous fluids, ·并且所述降低第三步骤(1003)包括改变所述流体穿过所述薄膜的流速的步骤。- and said reducing the third step (1003) comprises the step of changing the flow rate of said fluid through said membrane. 11.一种用于监控适合于进行工业方法(1000)的工业设备(9)的流体网络的流体(11)中的挥发性有机化合物的浓度的装置(10),所述流体(11)包含多种挥发性有机化合物,其特征在于所述装置包括:11. A device (10) for monitoring the concentration of volatile organic compounds in a fluid (11) of a fluid network of an industrial plant (9) suitable for carrying out an industrial process (1000), the fluid (11) comprising A variety of volatile organic compounds, characterized in that the device comprises: ·分析器(15),所述分析器位于所述流体网络中的第一位置(13)处,适合于在线测量所述第一位置(13)处所述流体(11)中的所述多种挥发性有机化合物中的每种挥发性有机化合物的浓度(16),an analyzer (15), located at a first location (13) in the fluid network, adapted to measure on-line the multiple in the fluid (11) at the first location (13) the concentration of each volatile organic compound in the volatile organic compounds (16), ·比较器(17),所述比较器适合于将由所述分析器(15)测量的所述多种有机化合物中的每种挥发性有机化合物的所述浓度(16)与针对每种挥发性有机化合物的预定义阈值(160)进行比较,a comparator (17) adapted to compare the concentration (16) of each volatile organic compound in the plurality of organic compounds measured by the analyzer (15) with the concentration (16) for each volatile organic compound A predefined threshold (160) for organic compounds is compared, ·校正单元(18),所述校正单元适合于如果由所述分析器(15)测量的所述多种有机化合物中的至少一种挥发性有机化合物的所述浓度(16)大于对应的预定义阈值(160)则降低所述流体(11)中的所述至少一种挥发性有机化合物的所述浓度(16)。a correction unit (18) adapted if the concentration (16) of at least one volatile organic compound of the plurality of organic compounds measured by the analyzer (15) is greater than the corresponding predetermined Defining a threshold (160) reduces the concentration (16) of the at least one volatile organic compound in the fluid (11). 12.根据权利要求11所述的监控装置(10),其特征在于所述校正单元(18)包括用于将具有降低所述至少一种挥发性有机化合物的所述浓度(16)的效果的产品注入所述流体网络的装置。12. A monitoring device (10) according to claim 11, characterized in that the correction unit (18) comprises a device which will have the effect of reducing the concentration (16) of the at least one volatile organic compound The means by which product is injected into the fluid network. 13.根据权利要求11和12中任一项所述的监控装置(10),其特征在于所述校正单元(18)包括第一控制模块,所述第一控制模块配置为作用于所述工业方法(1000)的至少一个参数(12),该至少一个参数具有根据所测量的所述至少一种挥发性有机化合物的浓度变化降低所述至少一种挥发性有机化合物的所述浓度(16)的效果。13. The monitoring device (10) according to any one of claims 11 and 12, characterized in that the correction unit (18) comprises a first control module configured to act on the industrial At least one parameter (12) of the method (1000), the at least one parameter having reducing the concentration (16) of the at least one volatile organic compound as a function of a change in the measured concentration of the at least one volatile organic compound Effect. 14.根据权利要求11至13中任一项所述的监控装置(10),其特征在于其包括远程传输装置,所述远程传输装置适合于将由所述分析器(15)测量的所述多种挥发性有机化合物中的每种挥发性有机化合物的所述浓度(16)远程传输至控制中心。14. Monitoring device (10) according to any one of claims 11 to 13, characterized in that it comprises a remote transmission device adapted to measure the polynomial measured by the analyzer (15) Said concentration (16) of each of the volatile organic compounds is transmitted remotely to a control center.
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Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT201900013506A1 (en) * 2019-07-31 2021-01-31 I L P A V S P A ECO-SUSTAINABLE SYSTEM AND METHOD FOR THE RECOVERY OF PLASTIC MATERIALS
US11881093B2 (en) 2020-08-20 2024-01-23 Denso International America, Inc. Systems and methods for identifying smoking in vehicles
US12269315B2 (en) 2020-08-20 2025-04-08 Denso International America, Inc. Systems and methods for measuring and managing odor brought into rental vehicles
US11932080B2 (en) 2020-08-20 2024-03-19 Denso International America, Inc. Diagnostic and recirculation control systems and methods
US11636870B2 (en) 2020-08-20 2023-04-25 Denso International America, Inc. Smoking cessation systems and methods
US12017506B2 (en) 2020-08-20 2024-06-25 Denso International America, Inc. Passenger cabin air control systems and methods
US11828210B2 (en) 2020-08-20 2023-11-28 Denso International America, Inc. Diagnostic systems and methods of vehicles using olfaction
US12377711B2 (en) 2020-08-20 2025-08-05 Denso International America, Inc. Vehicle feature control systems and methods based on smoking
US11760170B2 (en) 2020-08-20 2023-09-19 Denso International America, Inc. Olfaction sensor preservation systems and methods
US12251991B2 (en) 2020-08-20 2025-03-18 Denso International America, Inc. Humidity control for olfaction sensors
US11813926B2 (en) 2020-08-20 2023-11-14 Denso International America, Inc. Binding agent and olfaction sensor
US11760169B2 (en) 2020-08-20 2023-09-19 Denso International America, Inc. Particulate control systems and methods for olfaction sensors
FR3124744A1 (en) 2021-07-02 2023-01-06 Suez Groupe PROCESS FOR IN SITU REGENERATION OF AN ADSORBENT MEDIA
FR3124742A1 (en) 2021-07-02 2023-01-06 Suez Groupe ON-SITE ADSORBENT MEDIA REGENERATION PROCESS

Citations (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5733437A (en) * 1991-02-13 1998-03-31 Baker; Mark D. Method for detecting small molecules in aqueous liquids
US5777214A (en) * 1996-09-12 1998-07-07 Lockheed Martin Energy Research Corporation In-situ continuous water analyzing module
CN1345293A (en) * 1999-03-02 2002-04-17 美国过滤公司 Air and water purification using continuous breakpoint halogenation
US6485688B1 (en) * 2000-04-24 2002-11-26 General Electric Company On-line sparging sampling and monitoring systems and methods
CN101076723A (en) * 2003-07-11 2007-11-21 Pda安全解决方案有限公司 Remote monitoring system for water
JP2009199237A (en) * 2008-02-20 2009-09-03 Seiko Epson Corp Emission control management system, normal emission control management device, emergency emission control management device, emission control management method and emission control management program
US20090277255A1 (en) * 2008-05-07 2009-11-12 Gary Lynn Emmert Real-Time, On-Line Analysis for the Quantification of Trihalomethane Species Within Drinking Water Supplies
US20090290025A1 (en) * 2008-04-03 2009-11-26 Ahmet Enis Cetin Method, device and system for determining the presence of volatile organic compounds (voc) in video
US20100292844A1 (en) * 2009-05-14 2010-11-18 Omni Water Solutions Llc Self-contained portable multi-mode water treatment system and methods
CN102298368A (en) * 2011-06-17 2011-12-28 中国环境科学研究院 System for monitoring volatile organic contaminants in water source
CN102362037A (en) * 2009-03-24 2012-02-22 法国威立雅水务集团 Equipment and method for monitoring the quality of water in drinking water network
CN102735859A (en) * 2012-07-13 2012-10-17 力合科技(湖南)股份有限公司 Automatic online monitoring method and device for VOCs (volatile organic chemicals) in water
US20130029427A1 (en) * 2010-04-22 2013-01-31 Bolt, N.V. Methods and Apparatus for Determination of Halohydrocarbons
CN103675308A (en) * 2013-12-30 2014-03-26 力合科技(湖南)股份有限公司 On-line analyzer for aquatic VOCs (Volatile Organic Chemicals)
CN104136377A (en) * 2012-03-06 2014-11-05 纳尔科公司 Treatment of industrial water systems
CN105403679A (en) * 2015-10-30 2016-03-16 桂林市腾瑞电子科技有限公司 Monitoring system and monitoring method of water conditions in water reservoir
CN105473816A (en) * 2013-09-25 2016-04-06 哈利伯顿能源服务公司 Systems and methods for real time measurement of gas content in drilling fluids

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5435169A (en) * 1993-06-14 1995-07-25 New Jersey Institute Of Technology Continuous monitoring of organic pollutants
EP2710366A4 (en) * 2011-05-18 2014-12-03 Bolt N V Method and apparatus for determination of haloacetic acid ("haa") presence in aqueous solutions

Patent Citations (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5733437A (en) * 1991-02-13 1998-03-31 Baker; Mark D. Method for detecting small molecules in aqueous liquids
US5777214A (en) * 1996-09-12 1998-07-07 Lockheed Martin Energy Research Corporation In-situ continuous water analyzing module
CN1345293A (en) * 1999-03-02 2002-04-17 美国过滤公司 Air and water purification using continuous breakpoint halogenation
US6485688B1 (en) * 2000-04-24 2002-11-26 General Electric Company On-line sparging sampling and monitoring systems and methods
CN101076723A (en) * 2003-07-11 2007-11-21 Pda安全解决方案有限公司 Remote monitoring system for water
JP2009199237A (en) * 2008-02-20 2009-09-03 Seiko Epson Corp Emission control management system, normal emission control management device, emergency emission control management device, emission control management method and emission control management program
US20090290025A1 (en) * 2008-04-03 2009-11-26 Ahmet Enis Cetin Method, device and system for determining the presence of volatile organic compounds (voc) in video
US20090277255A1 (en) * 2008-05-07 2009-11-12 Gary Lynn Emmert Real-Time, On-Line Analysis for the Quantification of Trihalomethane Species Within Drinking Water Supplies
CN102362037A (en) * 2009-03-24 2012-02-22 法国威立雅水务集团 Equipment and method for monitoring the quality of water in drinking water network
US20100292844A1 (en) * 2009-05-14 2010-11-18 Omni Water Solutions Llc Self-contained portable multi-mode water treatment system and methods
US20130029427A1 (en) * 2010-04-22 2013-01-31 Bolt, N.V. Methods and Apparatus for Determination of Halohydrocarbons
CN102298368A (en) * 2011-06-17 2011-12-28 中国环境科学研究院 System for monitoring volatile organic contaminants in water source
CN104136377A (en) * 2012-03-06 2014-11-05 纳尔科公司 Treatment of industrial water systems
CN102735859A (en) * 2012-07-13 2012-10-17 力合科技(湖南)股份有限公司 Automatic online monitoring method and device for VOCs (volatile organic chemicals) in water
CN105473816A (en) * 2013-09-25 2016-04-06 哈利伯顿能源服务公司 Systems and methods for real time measurement of gas content in drilling fluids
CN103675308A (en) * 2013-12-30 2014-03-26 力合科技(湖南)股份有限公司 On-line analyzer for aquatic VOCs (Volatile Organic Chemicals)
CN105403679A (en) * 2015-10-30 2016-03-16 桂林市腾瑞电子科技有限公司 Monitoring system and monitoring method of water conditions in water reservoir

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
史高杨 主编: "《有机化学实验》", 31 August 2015, 合肥:合肥工业大学出版社 *
吕玉光 主编: "《仪器分析 在线学习版》", 31 January 2016, 北京:中国医药科技出版社 *
袁海勤 等: "长江饮用水源地 18 种挥发性有机物的自动监测应用研究", 《环境监控与预警》 *

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